EP1892044A1 - Elektrostatischer abscheider - Google Patents

Elektrostatischer abscheider Download PDF

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Publication number
EP1892044A1
EP1892044A1 EP05764928A EP05764928A EP1892044A1 EP 1892044 A1 EP1892044 A1 EP 1892044A1 EP 05764928 A EP05764928 A EP 05764928A EP 05764928 A EP05764928 A EP 05764928A EP 1892044 A1 EP1892044 A1 EP 1892044A1
Authority
EP
European Patent Office
Prior art keywords
adsorption
discharge
air
fine particles
plate
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
EP05764928A
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English (en)
French (fr)
Other versions
EP1892044A4 (de
EP1892044B1 (de
Inventor
Masatoshi Furuta
Shigenobu Ohkura
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Hidec Co Ltd
Zesu Giko Co Ltd
Original Assignee
Hidec Co Ltd
Zesu Giko Co Ltd
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Publication date
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Publication of EP1892044A1 publication Critical patent/EP1892044A1/de
Publication of EP1892044A4 publication Critical patent/EP1892044A4/de
Application granted granted Critical
Publication of EP1892044B1 publication Critical patent/EP1892044B1/de
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    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03C—MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03C3/00—Separating dispersed particles from gases or vapour, e.g. air, by electrostatic effect
    • B03C3/02—Plant or installations having external electricity supply
    • B03C3/04—Plant or installations having external electricity supply dry type
    • B03C3/08—Plant or installations having external electricity supply dry type characterised by presence of stationary flat electrodes arranged with their flat surfaces parallel to the gas stream
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03C—MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03C3/00—Separating dispersed particles from gases or vapour, e.g. air, by electrostatic effect
    • B03C3/34—Constructional details or accessories or operation thereof
    • B03C3/36—Controlling flow of gases or vapour
    • B03C3/361—Controlling flow of gases or vapour by static mechanical means, e.g. deflector
    • B03C3/363—Controlling flow of gases or vapour by static mechanical means, e.g. deflector located before the filter
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03C—MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03C3/00—Separating dispersed particles from gases or vapour, e.g. air, by electrostatic effect
    • B03C3/02—Plant or installations having external electricity supply
    • B03C3/04—Plant or installations having external electricity supply dry type
    • B03C3/10—Plant or installations having external electricity supply dry type characterised by presence of electrodes moving during separating action
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03C—MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03C3/00—Separating dispersed particles from gases or vapour, e.g. air, by electrostatic effect
    • B03C3/02—Plant or installations having external electricity supply
    • B03C3/16—Plant or installations having external electricity supply wet type
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03C—MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03C3/00—Separating dispersed particles from gases or vapour, e.g. air, by electrostatic effect
    • B03C3/34—Constructional details or accessories or operation thereof
    • B03C3/36—Controlling flow of gases or vapour
    • B03C3/361—Controlling flow of gases or vapour by static mechanical means, e.g. deflector
    • B03C3/365—Controlling flow of gases or vapour by static mechanical means, e.g. deflector located after the filter
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03C—MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03C3/00—Separating dispersed particles from gases or vapour, e.g. air, by electrostatic effect
    • B03C3/34—Constructional details or accessories or operation thereof
    • B03C3/40—Electrode constructions
    • B03C3/41—Ionising-electrodes
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03C—MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03C3/00—Separating dispersed particles from gases or vapour, e.g. air, by electrostatic effect
    • B03C3/34—Constructional details or accessories or operation thereof
    • B03C3/40—Electrode constructions
    • B03C3/45—Collecting-electrodes
    • B03C3/47—Collecting-electrodes flat, e.g. plates, discs, gratings
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03C—MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03C3/00—Separating dispersed particles from gases or vapour, e.g. air, by electrostatic effect
    • B03C3/34—Constructional details or accessories or operation thereof
    • B03C3/74—Cleaning the electrodes
    • B03C3/78—Cleaning the electrodes by washing
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A50/00—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
    • Y02A50/20—Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters
    • Y02A50/2351—Atmospheric particulate matter [PM], e.g. carbon smoke microparticles, smog, aerosol particles, dust

Definitions

  • the present invention relates to an electrostatic precipitator, in particular an electrostatic precipitator that is capable of collecting fine particles that have been charged by corona discharge by rotating adsorption plates.
  • the theory of dust collection by an electrostatic precipitator is defined here as follows: fine particles are electrically charged by a corona discharge that is generated by a discharge electrode; and these electrically charged fine particles are drawn and collected by a dust-collecting counter electrode by using the Coulomb force.
  • This electrostatic precipitator is characterized by notable advantages such as: 1) minimum pressure loss; 2) a large quantity gas processing capacity; and 3) a high rate of dust collection. Therefore, it is used in environments such as factories and power stations where a large quantity of contaminated air is released.
  • the electrostatic precipitator is commonly comprised of major structural components, i.e., a discharge electrode that is formed to have a large surface curvature, such as a needle or wire, to generate a corona discharge to charge fine particles; a collecting electrode, the counter electrode, which is formed into a plate to collect the charged particles; a rectifier to adjust the air flow in the electrostatic precipitator; a hammering device (dry type) and spray device (wet type) to separate the adhering fine particles from the dust-collecting electrode; a hopper that collects the separated particles; and attachments (an electrical power source for corona discharge and a charge control device).
  • a discharge electrode that is formed to have a large surface curvature, such as a needle or wire, to generate a corona discharge to charge fine particles
  • a collecting electrode the counter electrode, which is formed into a plate to collect the charged particles
  • a rectifier to adjust the air flow in the electrostatic precipitator
  • a hammering device dry type
  • the above-described hammering device is used in a dry-type electrostatic precipitator: it is used to hammer the dust-collecting electrode so that the fine particles that have been collected are shaken off and collected in the collecting means such as a hopper provided at the lower portion thereof.
  • the fine particles that have been collected in the dust-collecting electrode are washed off when a cleaning fluid such as water is sprayed.
  • a cleaning fluid such as water
  • the fine particles are removed from the collecting electrode by adopting a dry- and wet-type method, as described above.
  • a type in which the discharge and collecting electrodes are housed in an exchangeable cartridge is used.
  • the cartridge is replaced after many particles have been collected on the collecting electrode (which compromises the dust-collecting efficacy), thus maintaining a steady dust-colleting efficacy.
  • used cartridges are subjected to a particle-removing operation in a special apparatus provided by the manufacturer so that they may be recycled.
  • the apparatus is easily maintained, obviating the need to attach a dust-removing apparatus such as that described earlier, which contributes to down-sizing the entire apparatus and reducing production costs.
  • Patent Document 1 Unexamined Japanese Patent Publication No. 2003-126729
  • Patent Document 2 Unexamined Japanese Patent Publication No. 2004-141826
  • the present invention offers an electrostatic precipitator that is not compromised in its efficacy to collect fine particles in spite of continuous operation for a long time and is maintained easily by procedures such as cleansing.
  • the air-current generating means generates an air flow (air current) in the air duct: for example, by operating a propeller that is connected to driving device such as a motor, an air current is created in association with the rotation of the propeller.
  • driving device such as a motor
  • the amount of the airflow or flow velocity (flow rate) may be adjusted as desired.
  • the fine particles in the contaminated air are electrically charged by a discharge mechanism (to be elaborated later); and while in a charged state, are electrically adsorbed and collected by the adsorption surface of the adsorption plates at the opposing electrode with the aid of the Coulomb force.
  • the adsorption plates that comprise the collecting means rotate axially along with the adsorptive shaft by means of a plate rotating means.
  • the positional relationship between the fine particles contained in the contaminated air and the adsorptive surface undergoes changes by the minute.
  • the fine particles that are collected by the Coulomb force are generally evenly adsorbed over the entire adsorptive surface instead of being localized in specific areas on the adsorption surfaces of the adsorption plates.
  • the discharge means is intended to supply a corona discharge to charge the fine particles that are contained in the contaminated air. It comprises mainly a discharge shaft that is connected to the discharge voltage supplying means, charging plates and a discharge electrode.
  • the corona discharge occurs readily at the pointed section.
  • a discharge electrode that has a pointed end section at the end is used. Then, this pointed section is arranged to oppose the airflow or to face the inlet.
  • Each charging plate between the adsorption plates with a set interval in the direction of the width of the air duct, while a plurality of discharging electrodes are arranged along the edge opposing the suction inlet in the direction of the height of the housing.
  • a corona discharge is generated by the discharge voltage that is provided by the discharge voltage supplying means at the pointed ends of the discharge electrodes that constitute a discharge means.
  • contaminated air is taken through the inlet in the air duct and passes by some of the plurality of discharge electrodes that are arranged criss-crossing the outlet.
  • fine particles in the contaminated air are exposed to a corona discharge, which charges these particles (i.e., a positive charge).
  • the fine particles thus charged reach the space between the charging and adsorptive plates.
  • the discharge voltage supplying means has made the charging plates share the electrical charge of the charged particles, the particles are repelled by the Coulomb force as they approach the discharge surface of the charging plates and tend to move away from the discharge surface.
  • the adsorption plate has an electrical potential opposite that of the charged particles and it tends to adsorb these particles with the aid of the Coulomb force. Consequently, the particles that had been brought between the charging and absorption plates come under the repelling and absorptive effects, drawn to the absorption surface of the adsorption plate and collected.
  • the absorption plate is rotated by the plate rotating means that is connected to the adsorption shaft. Therefore, the positional relationship of the adsorption surface of the adsorption plate with the particles constantly changes, keeping the particles from accumulating in any specific site on the adsorption surface. In other words, the efficiency of adsorption and collection by the Coulomb force is not reduced by accumulated particles and the dust-collecting efficacy of the electrostatic precipitator is not compromised in a short period.
  • the electrostatic precipitator of the present invention may have the following embodiment: "t pointed end of the discharge electrode is set back at the side of the adsorption shaft away from the plate edge of the adsorption plate.”
  • the pointed ends of the discharge electrode are arranged away from the plate edge of the adsorption plate and toward the side of the adsorption shaft. Specifically, contaminated air, which has passed through the inlet, reaches between a pair of opposing adsorption plates and arrives at the charging plate where the discharge electrode is located. Because of the electrical field that has been formed by a supply of the discharge voltage from the pointed ends of the discharge electrode, a corona discharge is generated toward the adsorption surface of the adsorption plate. Thus, the contaminated air that has passed between the adsorption plates is exposed to this corona discharge.
  • the pointed means is set back on the side of the adsorption shaft, the particles that have been charged by the corona discharge are surrounded by the adsorption and charging plates. Consequently, the repulsive and adsorptive actions by the plates expedite trapping of the fine particles.
  • the electrostatic precipitator of the present invention may have the following features: "the air duct is sectioned by a first segment that is connected with the air duct and contains the discharge means and collecting means; a second segment to which the clean air that has been cleaned in the first segment is sent; and a third segment that houses the air flow generating means and exhausts the clean air sent from the second partition through the outlet.”
  • the air duct inside the housing is divided into 3 sections.
  • the air duct inside the housing is divided into 3 sections.
  • the air duct inside the housing is divided into 3 sections.
  • the air duct inside the housing is divided into 3 sections.
  • the fine particles are collected by means of the Coulomb force.
  • the second and third sections the cleansed air is released through the outlet.
  • the second section and the third sections that houses the airflow generating means are created.
  • the electrostatic precipitator of the present invention in addition to the embodiments shown above, may have the following features: "the pointed ends of the discharge electrode are arranged, while maintaining an equal distance from the adsorption surfaces of the pair of the adsorption plates with the pointed ends.”
  • the pointed ends of the discharge electrode are arranged with an equal distance from the absorption surface of each opposing absorption plate.
  • the condition for generating a corona discharge varies, depending on the distance from the pointed ends to absorption plates of different potentials. In other words, the smaller the distance between the pointed ends and the absorption plate, the more readily is the corona discharge generated.
  • the corona discharge is uniformly distributed on the absorption surface of both absorption plates.
  • a hole may be made where the discharge electrode may be inserted in the discharge plate and by inserting one end of the discharge electrode (corresponding to the side opposite the pointed end), the charge plate and the discharge electrode means may be built as a single unit, which makes it possible to maintain an equal distance from the absorption surface.
  • the means to charge fine particles with a corona discharge for the means to charge fine particles with a corona discharge, discharge electrodes with pointed ends, which are arranged at the charge plate and opposing edges of the charge plate toward the intake, are used.
  • discharge electrodes with pointed ends which are arranged at the charge plate and opposing edges of the charge plate toward the intake.
  • the fine particles contained in contaminated air can be effectively charged. Because the charged particles can be collected by the rotating adsorption plates while the particle absorption surface undergoes relative changes, fine particles do not accumulate in any specific place on the absorption surface. Consequently, the likelihood of attenuating the Coulomb force and reducing the collection efficacy is unlikely.
  • the structure of the electrostatic precipitator itself may be simplified and the maintenance (cleansing) operation of removing fine particles from the adsorptive surface can be conducted more simply than by the conventional method.
  • the pointed ends of the discharge electrode are arranged equidistance from the pair of adsorption plates so that the corona discharge does not occur unevenly on one adsorption plate.
  • FIG. 1 is an explanation view showing the internal structure of the electrostatic precipitator viewed from the side thereof;
  • FIG. 2 is an explanation view showing the internal structure of the electrostatic precipitator viewed from the top thereof;
  • FIG. 3 is an explanation view illustrating the structures of the discharge electrode means, charging plates and adsorption plates.
  • FIG. 4 is an explanation view showing the movement of the charged particles.
  • a collecting section 14 having generally a rod-shaped adsorption shaft 11 that runs horizontally for the width of the air duct 7 (corresponding to the right and left sides of FIG.
  • a discharge voltage supply section 25 that is electrically connected to a discharge axis 17 of the discharge section 24 and supplies the discharge voltage so that a corona discharge (CD) will occur at a sharp needle-like pointed ends 23; and washing fluid injection section 26 that is installed in the upper part inside air duct 7 and injects washing fluid 27 on each adsorption surface 12 of adsorption plates 13 to wash off fine particles 2 from the adsorptive surfaces 12.
  • the electrostatic precipitator 1 of this embodiment is explained in further detail below.
  • the housing 8 that is encased in a generally rectangular box has the inlet 4 that opens to a front side 8a of the housing and has the open outlet 6 at a housing back 8b opposite a housing front 8a.
  • the housing contains air duct 7 that connects the inlet 4 and the outlet 6. Starting at the inlet 4 and ending at the outlet 6, this air duct 7 is divided into 3 sections, 28a, 28b, and 28c.
  • first section 28a where the contaminated air taken in through the inlet 4 is guided to the discharge section 24 then to the collecting section 14; the second section 28b, located downstream from the first section 28a, smaller than the first section 28a to which the clean air 5 is sent; and the third section 28c that contains the aforementioned section 10 to generate an air flow and discharge clean air 5 that has been sent from the second section 28b through the outlet 6.
  • dividing walls 29a and 29b exist to section off these. Furthermore, openings 30a and 30b are created to allow the flow of the clean air 5 that has been cleansed through the section 28a and others.
  • multiple current plates 32 are installed to stabilize the flow of the clean air 5 that travels through adjoining sections (e.g., between the first section 28a and the second section 28b). As shown in FIG. 1 , between the first section 28a and the second section 28b, the current plates 32 are arranged to be sloped downward toward downstream, while between the second section 28b and the third section 28c, they are sloped upward toward downstream.
  • a current plates 32 with an identical structure and almost identical actions are located between the intake 4 and discharge the section 24 and the collecting section 14.
  • the current plates 32 at the inlet 4 guide contaminated air 3 that has been sucked in to flow downward at an angle downstream, creating a steady stream toward the area where the discharge electrodes 19 are arranged in a vertical direction.
  • the contaminated air 3 is dispersed within the air duct 7 and kept from reaching the outlet 6 without the effect of a corona discharge. Consequently, the collecting efficacy by the electrostatic precipitator 1 is improved.
  • the electrostatic precipitator 1 of the present invention has a sloped floor surface 31 that tilts the floor of the housing 8 in a certain direction (tilted downward toward downstream of the air duct 7).
  • the cleaning fluid 27 is jet-sprayed on the adsorption surface 12 with the aid of the aforementioned washing fluid spraying section 26 and the fine particles 2 are washed off, the cleaning fluid 27 containing the fine particles 2 that has reached the sloped floor surface 31 of the housing 8 is led to waste the fluid retaining section 34 at the lowest section along the sloped floor surface 31.
  • This waste fluid retaining section 34 has a drain (not shown in the figure) that discharges the retained cleaning fluid 27 to the outside of housing 8. This embodiment facilitates recovery of the cleaning fluid 27 after it has been used in cleansing.
  • pointed ends 23 at one end of the discharge electrode 19 that is installed on the charge plate 20 are located so that the ends are placed away from plate a edge section 33 that is located at the charge plate 20 and toward the adsorption axis 11; in other words, these pointed ends 23 are held between pairs of adsorption plates 13.
  • a corona discharge CD
  • the fine particles 2 that are charged by a corona discharge tend to revert readily from a charged state to a neutral state. In other words, the action by the Coulomb force gradually weakens after charging.
  • the adsorption plates 13 are arranged to be close around the pointed end 23 of discharge the electrode 19 so that the fine particles 2 can be collected before the action by the Coulomb force may be weakened.
  • the ends of the pointed ends 23 of the discharging electrodes 19 are arranged to be equidistant from the adsorption surface 12 of a pair of the adsorption plates 13 that are facing each other ( FIG. 3 ).
  • the support clamps 36 for suspension support are attached at four corners of the upper surface 35 of the housing to facilitate installation and moving of the electrostatic precipitator 1.
  • a discharge voltage of about 10.5 kV is supplied by the discharge voltage supply section 25 that is connected to the discharge section 24.
  • This discharge voltage is transmitted to discharge an electrode 19 via the discharge shaft 17 and the charging plate 20 and creates an electrical differential between the charge plate 20 and the adsorption plate 13, resulting in the development of the corona discharge CD at the pointed ends 23.
  • the components other than the discharge section 24, in particular, the collecting section 14 and the housing 8 are constructed with non-conductive substances such as insulating material 17a so that they will be electrically insulated from discharge means 24; and it is made certain that no discharge voltage is detected at sites other than discharge electrode 19 or no electrical leakage due to high voltage occurs.
  • the discharge electrode section 19 is buried in the charging plate 20 so that they can be produced as a single unit; but the present invention is by no means limited to this embodiment. As long as the discharge electrode section 19 is fixed while remaining equidistant to the adsorption surface 12, other structural embodiments may be adopted.
  • the charging plate 20 and the discharge electrode 19 are formed to match the height and the width of inlet 4, the contaminated air 3 that has been rectified by the current plate 32 and discharged most certainly passes near corona discharge CD generated by the discharge electrode section 19. Consequently, the charging efficiency of the fine particles 2 is raised. Contrary to rotating adsorption plate 13, the charging plate 20 is supported by the discharge axis 17 and the charging plate support axis 18 without rotation; therefore, at about the center of charging plate 20, penetrating a hole section 20a having a diameter greater than the axial diameter of the adsorption axis 11 has been created.
  • the collecting means 14 having the adsorption plate 13 rotates with the adsorption shaft 11.
  • the adsorption plate 13 can rotate.
  • the electrostatic precipitator 1 of this embodiment has the charging plate 20 and the discharge electrode section 19 fixated in the air duct 7; however, by rotating adsorption plate 13, it can change at will the positional relationship between the charged particles 2 and the adsorption surface 12 of the adsorption plate 13. Subsequently, the fine particles 2 do not adhere or accumulate at a specific site of the adsorption surface 12 of the adsorption plate 13.
  • the discharge section 24 that is connected to the discharge voltage supply section 25 causes corona discharge CD at the pointed ends 23 of the discharge electrodes 19, while the adsorption plate 13 is in an electrically corresponding state against the discharge electrode 19 with the aid of parts such as a grounding wire. Consequently, the fine particles 2 of the contaminated air 3 that have been positively charged by the action of the corona charge CD repel charging plate 20 having the same electrical potential and move in a direction away from the discharge surface 21, while the adsorption plate 13 that has an electrical charge opposite that of the charged fine particles 2 draws the fine particles 2 to the adsorption surface 12 or exerts an adsorptive action on these fine particles 2.
  • the electrostatic precipitator 1 of this embodiment is equipped with the cleaning fluid spraying section 26 to physically remove the fine particles 2 that have been adsorbed and collected on the adsorption surface 12 of the adsorption plate 13.
  • This cleaning fluid spraying section 26 contains the main body of the cleaning apparatus that is installed as if to straddle in the direction of the width of the air duct 7 and with a plurality of spray nozzles (not shown); and it sprays the cleaning fluid 27 from the end of the spray nozzles onto the adsorption surface 12 of the adsorption plate 13, washes off the fine particles 2 and performs a cleansing operation.
  • the corona discharge CD from the discharge electrode 19 is suspended and the adsorption plate 13 is controlled by the plate rotating motor 16 to rotate around the adsorption shaft 11 so that the cleaning fluid 27 may be sprayed evenly on the adsorption surface 12.
  • the adsorption plate 13 turns at a rotational frequency lower than when the fine particles 2 are collected with the aid of the Coulomb force.
  • the cleaning fluid 27 and the fine particles 2 that adhere to the adsorption surface 12 come under the influence of a centrifugal force, move toward the direction of rotation of the adsorption plate 13 and eventually scatter from the plate edge 33 toward the air duct 7.
  • the scattered cleaning fluid 27 and others drop immediately below because of the gravity and reach the sloped floor surface 31 of the housing 8.
  • the cleaning fluid 27 and others that are scattered in the first section 28a are hampered by dividing wall 29a adjacent to second section 28b and do not reach the second section 28b.
  • the current plate 32 that is arranged to slant downward aids in their move toward the sloped floor surface 31 of the housing 8.
  • the current plate 32 that is arranged obliquely and turning upward between the second section 28b and the third section 28c prevents the cleaning fluid and others from reaching the third section 28c.
  • the fine particles 2, which have adhered to the adsorption surface 12 are then removed, are isolated from the cleaned air 5 and exhausted through the outlet 6.
  • the air flow generator 10 is operated and the rotating fan is started by the fan-operating motor.
  • the contaminated air 3 is sucked into inlet 4 by the air flow generator 10; and the air flow 9 is generated in the air duct 7 to discharge this as the clean air 5 through the outlet 6.
  • the plate-rotating motor 16 that is connected to the adsorption shaft 11 of the collecting section 14 is operated; the discharge voltage supply section 25 is activated; and the corona discharge CD is created from a plurality of the discharge electrodes 19 via the discharge plate 20.
  • the air flow 9 is generated in the air duct 7 by the air flow generator 10.
  • the contaminated air 3 is sucked into the inlet 4.
  • the flow of the contaminated air 3 is rectified by the current plate 32 that is located the downstream from the inlet 4 and is led to the first section 28a where the discharge section 24 and the collecting section 14 are located.
  • the flow 9 of the contaminated air 3 that has been sucked in may become uneven and its direction may form into a turbulent pattern. It has been known that the air flow 9 is highly likely to be dispersed from the inlet 4 heading outward.
  • the discharge voltage (e.g., 10.5 kV) is supplied to discharge electrodes 19 from discharge voltage supplying means 25 via the discharge shaft 17 and the charging plate 20, while the adsorption plate 13 is electrically connected to a grounding wire that is buried in the ground surface via the adsorption shaft 11 and the housing 8. Consequently, a very large electrical field is formed between the discharge surface 21 and the adsorption surface 12.
  • the corona discharge CD is released from the pointed ends 23 of the discharge electrode 19 and the fine particles 2 that have passed around the corona discharge CD become electrically charged.
  • the adsorption plate 13 is rotating at a set rotation frequency (e.g., 500 rpm) with the adsorption shaft as its axis (see arrow A of Fig. 3 ).
  • a set rotation frequency e.g. 500 rpm
  • the position of the adsorption surface 12 (where fine particles 2 are repelled by the charging plate 20 then drawn by the Coulomb force) is constantly changing.
  • the fine particles 2 that have collected on the adsorption surface 12 are affected by a centrifugal force in the direction of the rotating periphery due to the rotation of the adsorption plate 13.
  • the fine particles 2, together with those particles around them move toward the circumference; and when the aforementioned centrifugal force exerts a stronger impact against the adsorptive force to the adsorption surface 12, the fine particles 2 are scattered away from the adsorption surface 12. Then, then fine particles 2 join those particles around them, gaining in weight and size over those when they were first collected. Consequently, it becomes difficult for them to float in the clean air 5 that has been purified and gravity causes them to drop toward the sloped floor surface 31 of the air duct 7.
  • the present embodiment can be operated for many hours without cleaning or exchanging the collecting section 14. Therefore it is suitable for use in the kitchen of a restaurant where long hours of operation are mandatory.
  • the pointed ends 23 of the discharge electrodes 19 are set back from the plate edge 33 of the adsorption plate 13 and toward the adsorption shaft 11; so the pointed ends 23 are surrounded by the adsorption plates 13 that oppose each other; and the fine particles 2 that have been charged by the corona discharge CD originating at the discharge electrodes 19 are collected immediately on the surrounding adsorption surface 12 of adsorption plate 13 that are close to the discharge electrodes 19. Consequently, the charged fine particles 2 are collected by the adsorption plate 13 without fail.
  • the fine particles 2 are kept from being sent to the sections 28b and 28c downstream by the current plates 32 of the openings 30a and 30b that are created in the sectioning walls 29a and 29b to divide the sections 28a, 28b, and 28c.
  • the purity of the clean air 5 that is released from the outlet 6 is further improved.
  • the electrostatic precipitator 1 of this embodiment is equipped with the cleansing fluid spraying means 26 that is capable of spraying the cleansing fluid 27 on the rotating adsorption plates 13.
  • the fine particles 2 that have been collected on the adsorption surfaces 12 can be washed off.
  • the manner of cleaning by using the cleansing fluid spraying section 26 and the cleansing solution 27 has already been stated so their explanation is omitted here.

Landscapes

  • Electrostatic Separation (AREA)
EP05764928.7A 2005-06-13 2005-06-13 Elektrostatischer abscheider Not-in-force EP1892044B1 (de)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
PCT/JP2005/010778 WO2006134627A1 (ja) 2005-06-13 2005-06-13 電気集塵器

Publications (3)

Publication Number Publication Date
EP1892044A1 true EP1892044A1 (de) 2008-02-27
EP1892044A4 EP1892044A4 (de) 2010-03-17
EP1892044B1 EP1892044B1 (de) 2015-08-05

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ID=37531999

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EP05764928.7A Not-in-force EP1892044B1 (de) 2005-06-13 2005-06-13 Elektrostatischer abscheider

Country Status (6)

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US (1) US7641718B2 (de)
EP (1) EP1892044B1 (de)
JP (1) JP4744520B2 (de)
KR (1) KR101074724B1 (de)
CN (1) CN100571882C (de)
WO (1) WO2006134627A1 (de)

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KR100891432B1 (ko) * 2009-02-24 2009-04-06 (주) 동문테크 백휠터의 바이브로스타백과 케이지
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US9422187B1 (en) 2015-08-21 2016-08-23 Corning Incorporated Laser sintering system and method for forming high purity, low roughness silica glass
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CN108273666A (zh) * 2018-03-30 2018-07-13 雷山县福尧茶叶有限公司 一种苗族茶叶除杂装置
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Also Published As

Publication number Publication date
US20090056551A1 (en) 2009-03-05
KR101074724B1 (ko) 2011-10-18
EP1892044A4 (de) 2010-03-17
JPWO2006134627A1 (ja) 2009-01-08
WO2006134627A1 (ja) 2006-12-21
CN101111318A (zh) 2008-01-23
EP1892044B1 (de) 2015-08-05
JP4744520B2 (ja) 2011-08-10
KR20080014723A (ko) 2008-02-14
CN100571882C (zh) 2009-12-23
US7641718B2 (en) 2010-01-05

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